US2708685A - Primary cell - Google Patents

Primary cell Download PDF

Info

Publication number
US2708685A
US2708685A US322913A US32291352A US2708685A US 2708685 A US2708685 A US 2708685A US 322913 A US322913 A US 322913A US 32291352 A US32291352 A US 32291352A US 2708685 A US2708685 A US 2708685A
Authority
US
United States
Prior art keywords
starch
cloth
separator
coated
electrolyte
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US322913A
Inventor
Joseph J Coleman
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Burgess Battery Co
Original Assignee
Burgess Battery Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Burgess Battery Co filed Critical Burgess Battery Co
Priority to US322913A priority Critical patent/US2708685A/en
Priority to GB32704/53A priority patent/GB733300A/en
Priority to ES0212388A priority patent/ES212388A1/en
Application granted granted Critical
Publication of US2708685A publication Critical patent/US2708685A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M6/00Primary cells; Manufacture thereof
    • H01M6/04Cells with aqueous electrolyte
    • H01M6/06Dry cells, i.e. cells wherein the electrolyte is rendered non-fluid
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409Separators, membranes or diaphragms characterised by the material
    • H01M50/411Organic material
    • H01M50/429Natural polymers
    • H01M50/4295Natural cotton, cellulose or wood
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409Separators, membranes or diaphragms characterised by the material
    • H01M50/44Fibrous material
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M6/00Primary cells; Manufacture thereof
    • H01M6/22Immobilising of electrolyte

Definitions

  • This inventionv relates to improvements in primary cells, and particularly to improvements in primary cells adapted for operation at low temperatures, by which is meant temperatures between F. and 60 F.
  • Patent 2,403,571 a cell is disclosed having zinc and carbon electrodes and a depolarizer mix composed of manganese dioxide and carbon.
  • an electrolyte is provided member composed of starch coated and impregnated L- cloth or fabric results in improved low temperature performance, specifically increased cell capacity. The reason for this superiority of cloth over paper as a separator material is not understood, and it is the more surprising because paperv is superior to cloth in cells operating at f' Y ordinary temperatures.
  • the primary cell illustrated is a dry cell of the cylindrical type.
  • the negative electrode is the open-top cylindrical zinc cup 10.
  • a layer 121 of suitable non-conductive electrolyteresista-nt material such as blotting paper, paper board, resin composition, heat-fusible wax or pitch, or the like.
  • the bibulous non-conductive layer 14 which, in accordance with the present invention, is composed of starch coated and impregnated cloth., and is moistened with liquid electrolyte, Layer 14 will be described more in detail hereinafter.
  • depolarizing mix 16 which may be the mixture used in yconventional dry cells composed of powdered ⁇ manganese dioxide and 2,708,685 Patented MayV 17, 1955l conductive material, such as carbon or graphite, said mixture being moistened with the liquid electrolyte of the cell.
  • the separating layer 14 extends above the mix body 16 and is folded inwardly on the top of said body.
  • the upright rod-shaped positive electrode 18 which may be composed of carbon and has the metal cap 20 upon its upper end.
  • the depolarizing body 16 when moistened with the electrolyte is plastic and is compacted in position, whereby it makes rm contact with the carbon rod 18 and the layer 14. Elements 16 and 18 together serve as the positive electrode of the'cell.
  • the layer 14 serves ⁇ as avv bibulous separating member'which prevents conductive contact between the mix 16 and the negative electrode 10 and at the same time absorbs electrolyte and makes possible the electrolytic action of the cell.
  • a washer 22 of non-conductive, electrolyte-resistant material such as paper or cardboard is spaced above the top of the depolarizing body 16, thereby providing the space 24 for the reception of 'gases or liquids which may be produced during the operation of the cell.
  • a cylindrical jacket 26 of non-conductive material such as cardboard surrounds the cylindrical wall of zinc cup 10 and extends a short distance above the top of the zinc cup,
  • a heat-fusible seal closure 2S which may be composed of wax or pitch, rests on washer 22 and makes an adhesive sealing joint with the carbon rod 18 and metal cap 20 and also with the upper portions of the zinc cup 10 and outer jacket 26.
  • the electrolyte may be composed of an aqueous solution containing lithium chloride as disclosed' in Patent 2,403,571.
  • electrolyte is meant the liquid electrolyte which is contained in both the layer 14 and the mix 16.
  • the electrolyte compound may consist of lithium chloride alone or lithium chloride in combination with one or both of ammonium chloride and zinc chloride. With lithium chloride alone, to 45 parts of LiCl to 100 parts by weight of water is satisfactory. When ammonium chloride and/ or zinc chloride are present, the following proportions are satisfactory:
  • the electrolyte may contain calcium chloride to impart low temperature performance as disclosed in Patent 2,569,491.
  • a suitable composition is as follows:
  • separator 14 is composedV of porous, exible cloth or fabric coated and impregnated with starch. Any thin, open-mesh, nonconducti-ve fabric with line meshes may be used. A light weight cotton fabric is preferred but other fabrics may be used. A fabric which has been used successfully is cotton print cloth having a thread count of 64-60 (64 warp and Woof threads to the inch). Another fabric which has been used successfully is a woven cotton fabric which resembles cheese cloth and has a thread count of 44-45.
  • Starch compositions for use in dry cells are known and any suitable starch composition may be used moistened with sufficient water or liquid electrolyte to. make a plastic paste. It'may be composed of any suitable cereal, such as wheat, corn, potato, tapioca, or the like, or it may be a mixture of several cereals.
  • The-cereal' may be in the form of a powdered starch or a mixture of starch and iour.
  • mercury available at the surfaceof the zinc negative electrode which is exposed to the electrolyte in order to inhibit local action at said electrode.
  • This may conveniently be accomplished by including a mercury compound in the starch composition applied to the cloth separator.
  • a mercury compound may be used which is soluble in water to a limited extent, i. e., not more than 0.1 gram per 100 grams of water, as is diclosed in United States Patent 2,598,226.
  • suitable compounds are mercurous chloride, mercurous bromide, mercurous iodide, mercurous sulfate and mercuric phosphate.
  • a small amount of the mercury compound is sufcient, an amount providing .O25 milligram of mercury per square centimeter of area of the separator being sufficient.
  • EX- amples of suitable starch compositions are as follows, the parts being by weight.
  • sucient water is added to make a fluid paste, preferably of the consistency of a paint, and the paste is preferably thoroughly mixed in a colloid mill to provide uniform consistency.
  • the paste is coated upon both sides of the cloth sheet by any suitable coating method, such as spraying, brushing or passing the sheet in contact with the upper portion of a rotating roll the lower portion of which is irnmersed in a body of the paste.
  • a suitable coating method such as spraying, brushing or passing the sheet in contact with the upper portion of a rotating roll the lower portion of which is irnmersed in a body of the paste.
  • Preferably several coatings are applied to each side of the sheet and the sheet is then dried.
  • the application is controlled so that the coated sheet carries approximately .004 to .008 gram of the composition, based on the dry weight of the ingredients, per square .centimeter of area of the sheet.
  • the starch composition fills the meshes of the sheet and is present asa coating on both surfaces thereof. At the meshes, the composition extends continuously through the sheet from the surface of one coating to the surface of the other.
  • the coated cloth is readilyvflexible, which is an advantage in handling an insertion in the cell.
  • the starch coated and impregnated cloth separator is inserted in the Zinc cup l in the dry condition, land after the mix 16, which is moistened with the liquid electrolyte, is compacted in place, the separator 14 absorbs electrolyte from the mix to provide a body of electrolyte in contact with the negative electrode and extending between said electrode and vthe mix body 16.
  • the mercury compound in theseparator progressively goes into solution in the electrolyte and becomes available at the surface of the negative electrode 10 where it serves to inhibit local action.
  • the starch composition was the same as in Example 1 in the foregoing and for one group of cells it was applied to the cloth first described in the foregoing, having a thread count of 64-60.
  • the same starch composition was applied to a battery paper, which is a commercially available kraft paper regularly used for dry cell separators.
  • the cells were subjected to the Army-Navy BA-3O test at a temperature of -40 F. In accordance with this test, two cells are connected in series with each other and a resistance of 13.33 ohms for 4 minutes each half hour, 10 hours per day, 5 days per week. The capacity is reckoned in days of total time from the start of the test until the closed circuit voltage has fallen to 1.87 volts for the two cells in series.
  • a number of the cells having the starch-coated paper separator exhibited an average capacity of 1.95 days, and a similar number of cells having the starch-coated cloth separator exhibited an average capacity of 3.32 days.
  • the superior capacity resulting from the use of cloth instead of paper for the material of the separator is evident from the foregoing data.
  • the use of starch-coated cloth does not provide the same advantage in cells designed for operation at ordinary temperatures, that is, temperatures above 0 F.
  • cells of the conventional Leclanch type not containing lithium chloride in the electrolyte when operated at ordinary temperatures those having paper separators exhibit capacity equal to or greater than those having cloth separators. Paper separators are extensively used in cells designed for operation at ordinary temperatures.
  • a bibulous separator between said electrodes comprising a sheet of non-conductive porous cloth coated and impregnated with starch.
  • an initially dry bibulous separator between said electrodes comprising a sheet of open-mesh, non-conductive cloth coated and impregnated with starch.
  • a bibulous separator between said electrodes comprising a sheet of non-conductive porous cloth coated and impregnated with starch, said separator carrying a mercury compound which is soluble in water to an extent not exceeding 0.1 gram per grams of water.
  • a bibulous separator between said electrodes comprising a sheet of open-mesh, non-conductive cloth coated and impregnated with starch.
  • a. bibulous separator between said depolarizing mix and said negative electrode comprising a sheet of openmesh, non-conductive cloth coated and impregnated with starch. f .6.
  • a bibulous separator between said electrodes comprising a sheet of open-mesh, non-conductive cloth coated and impregnated with starch.
  • a low temperature primary cell having a positive electrode, a negative electrode, and an electrolyte containing lithium chloride, a bibulous separator between said electrodes comprising a sheet of open-mesh, nonconductive cloth coated and impregnated with starch.
  • a bibulous separator between said electrodes comprising a sheet of open-mesh, nonconductive cloth coated and impregnated with starch.
  • a 10W temperature cell having a positive electrode, a negative electrode and a moist depolarizing mix between said electrodes, the method which comprises placing adjacent to the negative electrode a dry bibulous separator comprising a sheet of porous non-conductive cloth coated and impregnated with starch, and compacting said moist mix between said separator and said positive electrode, whereby moisture from said mix is absorbed by said separator and said starch becomes soft and gelatinous.

Landscapes

  • General Chemical & Material Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Wood Science & Technology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Primary Cells (AREA)
  • Cell Separators (AREA)
  • Battery Electrode And Active Subsutance (AREA)
  • Secondary Cells (AREA)
  • Electric Double-Layer Capacitors Or The Like (AREA)

Description

JQ .1. COLEMAN PRIMARY CELL May 1.7, 1955 Filed Nov. 28, 1952 United States Patent O PRIMARY CELL Joseph J. Coleman, Freeport, Ill., assignor to Burgess Battery Company, Freeport, lll., a corporation of Delaware l Application November28, 1952, Serial No. 322,913
9 Claims. (Cl. 1256-124) This inventionv relates to improvements in primary cells, and particularly to improvements in primary cells adapted for operation at low temperatures, by which is meant temperatures between F. and 60 F.
It is the object of the invention to provide a primary cell having improved performance characteristics in the low temperaturev range.
= In Patents Nos. 2,403,571 and 2,569,491 there vare disclosed primary cells of the Leclanch type which are adapted for operation at low temperatures, and it is to the improvement of cells of this character that the presi ent invention is directed.
In Patent 2,403,571, a cell is disclosed having zinc and carbon electrodes and a depolarizer mix composed of manganese dioxide and carbon. To adapt the cell for low temperature operation an electrolyte is provided member composed of starch coated and impregnated L- cloth or fabric results in improved low temperature performance, specifically increased cell capacity. The reason for this superiority of cloth over paper as a separator material is not understood, and it is the more surprising because paperv is superior to cloth in cells operating at f' Y ordinary temperatures.
To provide an understanding of the invention it will be described in connectionwith a specific embodiment 0f a primary cell. It is to be understood that such embodiment is illustrative only and that the invention is not limited to any particular structure.
Thefsingleiigureof the' accompanying drawing is a sectional view of a primary cell in accordance with the invention,
The primary cell illustrated is a dry cell of the cylindrical type. The negative electrode is the open-top cylindrical zinc cup 10. Upon the bottom of cup 10 is disposed a layer 121 of suitable non-conductive electrolyteresista-nt material such as blotting paper, paper board, resin composition, heat-fusible wax or pitch, or the like. Against the interior cylindrical surface of the Zinc cup 10 is arranged the bibulous non-conductive layer 14 which, in accordance with the present invention, is composed of starch coated and impregnated cloth., and is moistened with liquid electrolyte, Layer 14 will be described more in detail hereinafter. Within the cup 10 and resting on bottom layer 12 and in contact with cylindrical ylayer 14 is the compressed body of depolarizing mix 16 which may be the mixture used in yconventional dry cells composed of powdered `manganese dioxide and 2,708,685 Patented MayV 17, 1955l conductive material, such as carbon or graphite, said mixture being moistened with the liquid electrolyte of the cell. As shown in the drawing, the separating layer 14 extends above the mix body 16 and is folded inwardly on the top of said body. v Embedded centrally in the depolarizing body 16 is the upright rod-shaped positive electrode 18 which may be composed of carbon and has the metal cap 20 upon its upper end.
The depolarizing body 16 when moistened with the electrolyte is plastic and is compacted in position, whereby it makes rm contact with the carbon rod 18 and the layer 14. Elements 16 and 18 together serve as the positive electrode of the'cell. The layer 14 serves` as avv bibulous separating member'which prevents conductive contact between the mix 16 and the negative electrode 10 and at the same time absorbs electrolyte and makes possible the electrolytic action of the cell.
A washer 22 of non-conductive, electrolyte-resistant material such as paper or cardboard is spaced above the top of the depolarizing body 16, thereby providing the space 24 for the reception of 'gases or liquids which may be produced during the operation of the cell. A cylindrical jacket 26 of non-conductive material such as cardboard surrounds the cylindrical wall of zinc cup 10 and extends a short distance above the top of the zinc cup, A heat-fusible seal closure 2S, which may be composed of wax or pitch, rests on washer 22 and makes an adhesive sealing joint with the carbon rod 18 and metal cap 20 and also with the upper portions of the zinc cup 10 and outer jacket 26.
The electrolyte may be composed of an aqueous solution containing lithium chloride as disclosed' in Patent 2,403,571. By electrolyte is meant the liquid electrolyte which is contained in both the layer 14 and the mix 16. ,The electrolyte compound may consist of lithium chloride alone or lithium chloride in combination with one or both of ammonium chloride and zinc chloride. With lithium chloride alone, to 45 parts of LiCl to 100 parts by weight of water is satisfactory. When ammonium chloride and/ or zinc chloride are present, the following proportions are satisfactory:
Parts by weight The electrolyte may contain calcium chloride to impart low temperature performance as disclosed in Patent 2,569,491. A suitable composition is as follows:
Parts by weight Water 40 to 65 CaCl2.2H2O 10t'o 30 NH4Cl 5 to 20 ZnClz 10 to 40 In accordance with the present invention, separator 14 is composedV of porous, exible cloth or fabric coated and impregnated with starch. Any thin, open-mesh, nonconducti-ve fabric with line meshes may be used. A light weight cotton fabric is preferred but other fabrics may be used. A fabric which has been used successfully is cotton print cloth having a thread count of 64-60 (64 warp and Woof threads to the inch). Another fabric which has been used successfully is a woven cotton fabric which resembles cheese cloth and has a thread count of 44-45.
Starch compositions for use in dry cells are known and any suitable starch composition may be used moistened with sufficient water or liquid electrolyte to. make a plastic paste. It'may be composed of any suitable cereal, such as wheat, corn, potato, tapioca, or the like, or it may be a mixture of several cereals. The-cereal' may be in the form of a powdered starch or a mixture of starch and iour.
In the cell of the invention it is preferred to have mercury available at the surfaceof the zinc negative electrode which is exposed to the electrolyte in order to inhibit local action at said electrode. This may conveniently be accomplished by including a mercury compound in the starch composition applied to the cloth separator. A mercury compound may be used which is soluble in water to a limited extent, i. e., not more than 0.1 gram per 100 grams of water, as is diclosed in United States Patent 2,598,226. Examples of suitable compounds are mercurous chloride, mercurous bromide, mercurous iodide, mercurous sulfate and mercuric phosphate. A small amount of the mercury compound is sufcient, an amount providing .O25 milligram of mercury per square centimeter of area of the separator being sufficient. EX- amples of suitable starch compositions are as follows, the parts being by weight.
In each case sucient water is added to make a fluid paste, preferably of the consistency of a paint, and the paste is preferably thoroughly mixed in a colloid mill to provide uniform consistency.
The paste is coated upon both sides of the cloth sheet by any suitable coating method, such as spraying, brushing or passing the sheet in contact with the upper portion of a rotating roll the lower portion of which is irnmersed in a body of the paste. Preferably several coatings are applied to each side of the sheet and the sheet is then dried. The application is controlled so that the coated sheet carries approximately .004 to .008 gram of the composition, based on the dry weight of the ingredients, per square .centimeter of area of the sheet. The starch composition fills the meshes of the sheet and is present asa coating on both surfaces thereof. At the meshes, the composition extends continuously through the sheet from the surface of one coating to the surface of the other. The coated cloth is readilyvflexible, which is an advantage in handling an insertion in the cell. In the assembly of the cell, the starch coated and impregnated cloth separator is inserted in the Zinc cup l in the dry condition, land after the mix 16, which is moistened with the liquid electrolyte, is compacted in place, the separator 14 absorbs electrolyte from the mix to provide a body of electrolyte in contact with the negative electrode and extending between said electrode and vthe mix body 16. The mercury compound in theseparator progressively goes into solution in the electrolyte and becomes available at the surface of the negative electrode 10 where it serves to inhibit local action.
In order to show the superior properties imparted to the low temperature cell by the use of the starch coated cloth separator, data are given hereinafter for cellsusing starch coated cloth and starch coated paper. I'he cells were of the same construction except for the material of the separator. They were of the cylindrical type described hereinbefore and of the ashlight size, i. e., having a. diameter of 11A inches and a height of 2% inches. depolarizing mix was composed of 87.5 parts of manganese dioxide and 12.5 parts of thermal acetylene black. The mix was moistened with liquid electrolyte of the following approximate composition, in parts by weight Ammonium chloride 7 Zinc chloride 14 Thel 4 Lithium chloride 15 Chromium trioxide 0.4 Water 63.6
The starch composition was the same as in Example 1 in the foregoing and for one group of cells it was applied to the cloth first described in the foregoing, having a thread count of 64-60. For the other group of cells the same starch composition was applied to a battery paper, which is a commercially available kraft paper regularly used for dry cell separators. The cells were subjected to the Army-Navy BA-3O test at a temperature of -40 F. In accordance with this test, two cells are connected in series with each other and a resistance of 13.33 ohms for 4 minutes each half hour, 10 hours per day, 5 days per week. The capacity is reckoned in days of total time from the start of the test until the closed circuit voltage has fallen to 1.87 volts for the two cells in series.
A number of the cells having the starch-coated paper separator exhibited an average capacity of 1.95 days, and a similar number of cells having the starch-coated cloth separator exhibited an average capacity of 3.32 days. The superior capacity resulting from the use of cloth instead of paper for the material of the separator is evident from the foregoing data. As has been stated heretofore, the use of starch-coated cloth does not provide the same advantage in cells designed for operation at ordinary temperatures, that is, temperatures above 0 F. With respect to cells of the conventional Leclanch type not containing lithium chloride in the electrolyte, when operated at ordinary temperatures those having paper separators exhibit capacity equal to or greater than those having cloth separators. Paper separators are extensively used in cells designed for operation at ordinary temperatures.
What is claimed is:
1. In a low temperature primary cell having a positive electrode and a negative electrode, a bibulous separator between said electrodes comprising a sheet of non-conductive porous cloth coated and impregnated with starch.
2. In a low temperature primary cell having a positive electrode and a negative electrode, an initially dry bibulous separator between said electrodes comprising a sheet of open-mesh, non-conductive cloth coated and impregnated with starch.
3. In a low temperature primary cell having a positive electrode and a negative electrode, a bibulous separator between said electrodes comprising a sheet of non-conductive porous cloth coated and impregnated with starch, said separator carrying a mercury compound which is soluble in water to an extent not exceeding 0.1 gram per grams of water.
4. In a low temperature primary cell having a positive electrode and a zinc negative electrode, a bibulous separator between said electrodes comprising a sheet of open-mesh, non-conductive cloth coated and impregnated with starch.
5. In a low temperature primary cell having a positive electrode, a zinc negative electrode and a depolarizing mix, a. bibulous separator between said depolarizing mix and said negative electrode comprising a sheet of openmesh, non-conductive cloth coated and impregnated with starch. f .6. In a low temperature primary cell having `a positive electrode, a negative electrode, and an electrolyte containing a compound from the group consisting of lithium chloride and calcium chloride, a bibulous separator between said electrodes comprising a sheet of open-mesh, non-conductive cloth coated and impregnated with starch.
7. ln a low temperature primary cell having a positive electrode, a negative electrode, and an electrolyte containing lithium chloride, a bibulous separator between said electrodes comprising a sheet of open-mesh, nonconductive cloth coated and impregnated with starch.
8. In a low temperature primary cell having a positive electrode, .a negative electrode, and an electrolyte containing calcium chloride, a bibulous separator between said electrodes comprising a sheet of open-mesh, nonconductive cloth coated and impregnated with starch.
9. 1n making a 10W temperature cell having a positive electrode, a negative electrode and a moist depolarizing mix between said electrodes, the method which comprises placing adjacent to the negative electrode a dry bibulous separator comprising a sheet of porous non-conductive cloth coated and impregnated with starch, and compacting said moist mix between said separator and said positive electrode, whereby moisture from said mix is absorbed by said separator and said starch becomes soft and gelatinous.
References Cited in the le of this patent UNITED STATES PATENTS 495,196 Barrett June 11, 1889 1,140,826 Hoppie May 25, 1915 1,400,513 Benner Dec. 20, 1921 2,403,571 Wilke July 9, 1946 2,569,491 Otto Oct. 2, 1951

Claims (1)

1. IN A LOW TEMPERATURE PRIMARY CELL HAVING A POSITIVE ELECTRODE AND A NEGATIVE ELECTRODE, A BIBULOUS SEPARATOR BETWEEN SAID ELECTRODES COMPRISING A SHEET OF NON-CONDUCTIVE POROUS CLOTH COATED AND IMPREGNATED WITH STARCH.
US322913A 1952-11-28 1952-11-28 Primary cell Expired - Lifetime US2708685A (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
US322913A US2708685A (en) 1952-11-28 1952-11-28 Primary cell
GB32704/53A GB733300A (en) 1952-11-28 1953-11-25 Improvements in or relating to primary electric cells
ES0212388A ES212388A1 (en) 1952-11-28 1953-11-27 Primary cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US322913A US2708685A (en) 1952-11-28 1952-11-28 Primary cell

Publications (1)

Publication Number Publication Date
US2708685A true US2708685A (en) 1955-05-17

Family

ID=23256985

Family Applications (1)

Application Number Title Priority Date Filing Date
US322913A Expired - Lifetime US2708685A (en) 1952-11-28 1952-11-28 Primary cell

Country Status (3)

Country Link
US (1) US2708685A (en)
ES (1) ES212388A1 (en)
GB (1) GB733300A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3973995A (en) * 1970-09-29 1976-08-10 Toshiso Kamai Leak proof dry cell
US4038466A (en) * 1975-08-27 1977-07-26 Leonid Lavrentievich Belyshev Method of producing thickened electrolyte for primary cell

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US405196A (en) * 1889-06-11 Galvanic battery
US1140826A (en) * 1914-06-24 1915-05-25 Hoppie Electrical Appliance Company Electrical battery.
US1400513A (en) * 1920-05-05 1921-12-20 Nat Carbon Co Inc Electric battery
US2403571A (en) * 1943-12-31 1946-07-09 Burgess Battery Co Dry cell
US2569491A (en) * 1946-06-27 1951-10-02 Earl M Otto Dry cell composition

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US405196A (en) * 1889-06-11 Galvanic battery
US1140826A (en) * 1914-06-24 1915-05-25 Hoppie Electrical Appliance Company Electrical battery.
US1400513A (en) * 1920-05-05 1921-12-20 Nat Carbon Co Inc Electric battery
US2403571A (en) * 1943-12-31 1946-07-09 Burgess Battery Co Dry cell
US2569491A (en) * 1946-06-27 1951-10-02 Earl M Otto Dry cell composition

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3973995A (en) * 1970-09-29 1976-08-10 Toshiso Kamai Leak proof dry cell
US4038466A (en) * 1975-08-27 1977-07-26 Leonid Lavrentievich Belyshev Method of producing thickened electrolyte for primary cell

Also Published As

Publication number Publication date
GB733300A (en) 1955-07-06
ES212388A1 (en) 1954-04-01

Similar Documents

Publication Publication Date Title
US2798895A (en) Point contact battery
GB634281A (en) Improvements in or relating to a deferred action primary electric battery
US2903498A (en) Primary dry cell
GB1490199A (en) Electrolytic cells
US2612533A (en) Primary cell
US2606941A (en) Primary cell and battery
US4248945A (en) Dry cell battery
US3961985A (en) Nickel-zinc cell
US2554447A (en) Voltaic cell
US2399127A (en) Dry cell
US2403571A (en) Dry cell
US2708685A (en) Primary cell
US1548539A (en) Process of making battery elements and products thereof
US3306781A (en) Depolarizer mixture and molded bodies
USRE23883E (en) Cuprous chloride electrodes
US2526789A (en) Dry cell
US2180839A (en) Primary cell
US3905834A (en) Dry cell
US3392057A (en) Air cell including zinc anode and alkali zincate electrolyte
US2923757A (en) Dry cell
US3996068A (en) Primary dry cell
US2542934A (en) Dry cell construction
US2586426A (en) Galvanic primary cell
US2814664A (en) Electric current producing cell
US1654038A (en) Lining for dry cells